US5429760A - Refrigerant composition containing trifluoromethane and 1,1,1,2-tetrafluoroethane - Google Patents
Refrigerant composition containing trifluoromethane and 1,1,1,2-tetrafluoroethane Download PDFInfo
- Publication number
- US5429760A US5429760A US08/089,829 US8982993A US5429760A US 5429760 A US5429760 A US 5429760A US 8982993 A US8982993 A US 8982993A US 5429760 A US5429760 A US 5429760A
- Authority
- US
- United States
- Prior art keywords
- refrigerant
- weight
- tetrafluoroethane
- trifluoromethane
- compressor
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000003507 refrigerant Substances 0.000 title claims abstract description 30
- 239000000203 mixture Substances 0.000 title claims abstract description 23
- XPDWGBQVDMORPB-UHFFFAOYSA-N Fluoroform Chemical compound FC(F)F XPDWGBQVDMORPB-UHFFFAOYSA-N 0.000 title claims abstract description 20
- LVGUZGTVOIAKKC-UHFFFAOYSA-N 1,1,1,2-tetrafluoroethane Chemical compound FCC(F)(F)F LVGUZGTVOIAKKC-UHFFFAOYSA-N 0.000 title claims abstract description 10
- 238000004378 air conditioning Methods 0.000 claims abstract description 9
- 238000005057 refrigeration Methods 0.000 claims description 10
- 238000000034 method Methods 0.000 claims description 8
- 230000008020 evaporation Effects 0.000 claims description 5
- 238000001704 evaporation Methods 0.000 claims description 5
- 238000012360 testing method Methods 0.000 description 9
- 238000005259 measurement Methods 0.000 description 5
- VOPWNXZWBYDODV-UHFFFAOYSA-N Chlorodifluoromethane Chemical compound FC(F)Cl VOPWNXZWBYDODV-UHFFFAOYSA-N 0.000 description 3
- 238000009835 boiling Methods 0.000 description 2
- 238000009833 condensation Methods 0.000 description 2
- 238000010586 diagram Methods 0.000 description 2
- 230000006835 compression Effects 0.000 description 1
- 238000007906 compression Methods 0.000 description 1
- 238000007710 freezing Methods 0.000 description 1
- 230000008014 freezing Effects 0.000 description 1
- 239000007788 liquid Substances 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000002360 preparation method Methods 0.000 description 1
- 238000000638 solvent extraction Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000012546 transfer Methods 0.000 description 1
- 238000011144 upstream manufacturing Methods 0.000 description 1
Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K5/00—Heat-transfer, heat-exchange or heat-storage materials, e.g. refrigerants; Materials for the production of heat or cold by chemical reactions other than by combustion
- C09K5/02—Materials undergoing a change of physical state when used
- C09K5/04—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa
- C09K5/041—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems
- C09K5/044—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds
- C09K5/045—Materials undergoing a change of physical state when used the change of state being from liquid to vapour or vice versa for compression-type refrigeration systems comprising halogenated compounds containing only fluorine as halogen
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2205/00—Aspects relating to compounds used in compression type refrigeration systems
- C09K2205/22—All components of a mixture being fluoro compounds
-
- C—CHEMISTRY; METALLURGY
- C09—DYES; PAINTS; POLISHES; NATURAL RESINS; ADHESIVES; COMPOSITIONS NOT OTHERWISE PROVIDED FOR; APPLICATIONS OF MATERIALS NOT OTHERWISE PROVIDED FOR
- C09K—MATERIALS FOR MISCELLANEOUS APPLICATIONS, NOT PROVIDED FOR ELSEWHERE
- C09K2205/00—Aspects relating to compounds used in compression type refrigeration systems
- C09K2205/40—Replacement mixtures
- C09K2205/43—Type R22
-
- F—MECHANICAL ENGINEERING; LIGHTING; HEATING; WEAPONS; BLASTING
- F25—REFRIGERATION OR COOLING; COMBINED HEATING AND REFRIGERATION SYSTEMS; HEAT PUMP SYSTEMS; MANUFACTURE OR STORAGE OF ICE; LIQUEFACTION SOLIDIFICATION OF GASES
- F25D—REFRIGERATORS; COLD ROOMS; ICE-BOXES; COOLING OR FREEZING APPARATUS NOT OTHERWISE PROVIDED FOR
- F25D2400/00—General features of, or devices for refrigerators, cold rooms, ice-boxes, or for cooling or freezing apparatus not covered by any other subclass
- F25D2400/30—Quick freezing
Definitions
- the present invention relates to novel compositions containing trifluoromethane and 1,1,1,2-tetrafluoroethane which are useful as refrigerants in refrigerating machines and air-conditioning systems.
- the object of the invention is therefore to provide a suitable refrigerant for such refrigerating machines and air-conditioning systems.
- a refrigerant composition consisting of from 2 to 8% by weight trifluoromethane and from 92 to 98% by weight 1,1,1,2-tetrafluoroethane.
- FIG. 1 is a diagram of a compressor test stand (CO: compressor, LF: water-cooled liquefier, RE: restrictor, EV: expansion valve, MI: mixing tube, VO: volume- flow meter, A, B: branching points, I: inlet valve).
- CO compressor
- LF water-cooled liquefier
- RE restrictor
- EV expansion valve
- MI mixing tube
- VO volume- flow meter
- A, B branching points
- I inlet valve
- Particularly preferred in this context are compositions containing R23 in an amount from 4 to 6% by weight.
- compositions according to the invention are advantageously suitable, in particular, as refrigerants for the medium and low temperature range with evaporation temperatures (t 0 ) below -25° C., for example as refrigerants for the temperature range with t 0 between -25° C. to -45° C. in refrigerating machines such as, for example, upright freezers, chest freezers, cold chambers for aeronautical and scientific purposes or cold chambers for the rapid freezing of food, refrigeration plants for food markets, industrial large-scale refrigeration plants and air-conditioning appliances.
- refrigerants for the medium and low temperature range with evaporation temperatures (t 0 ) below -25° C. for example as refrigerants for the temperature range with t 0 between -25° C. to -45° C.
- refrigerating machines such as, for example, upright freezers, chest freezers, cold chambers for aeronautical and scientific purposes or cold chambers for the rapid freezing of food, refrigeration plants for food markets, industrial large-scale refrigeration plants and air-conditioning appliances
- a pressure vessel was evacuated using a vacuum pump and then cooled down in a commercially available chest freezer to approximately -25° C. With the aid of a balance, the calculated amount of the higher-boiling component R134a was first metered into the pressure vessel, followed by the lower-boiling component R23.
- a composition was produced which consisted of 95% by weight of R134a and 5% by weight of R23.
- the compressor test stand works according to the partial-condensation method and comprises a circulation system which contains a compressor CO, a liquefier LF, a restrictor RE, an inlet valve I, an expansion valve EV, a mixing tube MI and a volume-flow meter VO, connected to one another via conduits.
- the important stations of the compressor test stand used are shown diagrammatically in FIG. 1.
- the pressure vessel containing the refrigerant was connected to the inlet valve, upstream of the expansion valve, of the evacuated compressor test stand. In order to transfer the refrigerant in liquid form into the evacuated refrigeration system, the pressure vessel was reheated to room temperature. The measurements were then carried out at the compressor test stand to determine the refrigeration characteristics according to the partial-condensation method. The measurements were carried out according to the standard specifications DIN 8977 and ISO 917.
- the method is based on partitioning the refrigerant gas stream leaving the compressor CO at the branching point A into a refrigerant stream to be liquefied and a refrigerant stream to be throttled, which are recombined in point B after the mixture coming from the liquefier LF has been re-expanded via the expansion valve EV.
- a mixing tube MI evaporation of the liquefied refrigerant proportion and mixing with the gas stream coming from the restrictor RE takes place.
- the data measured are the temperatures and pressures at the inlet into the compressor (t 1h , p 0 ) and at the outlet from the compressor (t 2h , p c ), the effective volume flow V eff and the rotational speed of the compressor shaft.
- composition according to the invention which contains R23 and R134a and which forms a non-azeotropic mixture, was additionally subjected in a known manner to p-v-T-x measurements according to the isochor principle. Taking into account the volumetric behavior data, obtained from the p-v-T-x measurements, of the composition according to the invention, and the test results on the compressor test stand, it was possible to determine or calculate, in a known manner via the compilation of the Mollier diagram, the following refrigeration characteristics for the refrigerant composition according to the invention:
- the data determined on the basis of experimental measurements documents the useful refrigeration characteristics of the compositions according to the invention comprising R23 and R134a.
- a high refrigerating capacity and a high performance coefficient are achieved at an acceptable pressure ratio.
Landscapes
- Chemical & Material Sciences (AREA)
- Engineering & Computer Science (AREA)
- Physics & Mathematics (AREA)
- Chemical Kinetics & Catalysis (AREA)
- Combustion & Propulsion (AREA)
- Thermal Sciences (AREA)
- Materials Engineering (AREA)
- Organic Chemistry (AREA)
- Organic Low-Molecular-Weight Compounds And Preparation Thereof (AREA)
- Lubricants (AREA)
- Fats And Perfumes (AREA)
Abstract
Compositions containing trifluoromethane and 1,1,1,2-tetrafluoroethane which are useful as refrigerants in refrigerating machines and air-conditioning systems.
Description
The present invention relates to novel compositions containing trifluoromethane and 1,1,1,2-tetrafluoroethane which are useful as refrigerants in refrigerating machines and air-conditioning systems.
In air-conditioning systems and refrigerating machines for the medium and low temperature range, the refrigerant chlorodifluoromethane (=R22) has hitherto been used in many cases. For ecological reasons, the use of the refrigerant R22 is now no longer desirable.
The object of the invention is therefore to provide a suitable refrigerant for such refrigerating machines and air-conditioning systems.
This and other objects of the invention are achieved by providing a refrigerant composition consisting of from 2 to 8% by weight trifluoromethane and from 92 to 98% by weight 1,1,1,2-tetrafluoroethane.
The invention will be described in further detail hereinafter with reference to the accompanying drawing in which:
FIG. 1 is a diagram of a compressor test stand (CO: compressor, LF: water-cooled liquefier, RE: restrictor, EV: expansion valve, MI: mixing tube, VO: volume- flow meter, A, B: branching points, I: inlet valve).
Compositions containing trifluoromethane (=R23) and 1,1,1,2-tetrafluoroethane (=R134a) have now been found which are suitable as refrigerants for refrigerating machines and air-conditioning systems.
The invention therefore relates to compositions which are suitable as refrigerants in refrigerating machines and air-conditioning systems and which comprise from 2 to 8% by weight of trifluoromethane (=R23) and from 92 to 98% by weight of 1,1,1,2-tetrafluoroethane (=R134a) and to their use as refrigerants in refrigerating machines and air-conditioning systems. Particularly preferred in this context are compositions containing R23 in an amount from 4 to 6% by weight.
The compositions according to the invention are advantageously suitable, in particular, as refrigerants for the medium and low temperature range with evaporation temperatures (t0) below -25° C., for example as refrigerants for the temperature range with t0 between -25° C. to -45° C. in refrigerating machines such as, for example, upright freezers, chest freezers, cold chambers for aeronautical and scientific purposes or cold chambers for the rapid freezing of food, refrigeration plants for food markets, industrial large-scale refrigeration plants and air-conditioning appliances.
The following examples are intended to illustrate the invention in further detail without limiting its scope.
Preparation of a Refrigerant Composition From R23 and R134a
A pressure vessel was evacuated using a vacuum pump and then cooled down in a commercially available chest freezer to approximately -25° C. With the aid of a balance, the calculated amount of the higher-boiling component R134a was first metered into the pressure vessel, followed by the lower-boiling component R23. A composition was produced which consisted of 95% by weight of R134a and 5% by weight of R23.
Refrigeration Characteristics of a Refrigerant Composition Comprising R23 and R134a
Using the refrigerant composition prepared according to Example 1, comprising 5% by weight of R23 and 95% by weight of R134a, tests were carried out on a known type of compressor test stand (manufactured by Copeland) to determine the refrigeration characteristics. The compressor test stand works according to the partial-condensation method and comprises a circulation system which contains a compressor CO, a liquefier LF, a restrictor RE, an inlet valve I, an expansion valve EV, a mixing tube MI and a volume-flow meter VO, connected to one another via conduits. The important stations of the compressor test stand used are shown diagrammatically in FIG. 1.
The pressure vessel containing the refrigerant was connected to the inlet valve, upstream of the expansion valve, of the evacuated compressor test stand. In order to transfer the refrigerant in liquid form into the evacuated refrigeration system, the pressure vessel was reheated to room temperature. The measurements were then carried out at the compressor test stand to determine the refrigeration characteristics according to the partial-condensation method. The measurements were carried out according to the standard specifications DIN 8977 and ISO 917. The method is based on partitioning the refrigerant gas stream leaving the compressor CO at the branching point A into a refrigerant stream to be liquefied and a refrigerant stream to be throttled, which are recombined in point B after the mixture coming from the liquefier LF has been re-expanded via the expansion valve EV. In a mixing tube MI, evaporation of the liquefied refrigerant proportion and mixing with the gas stream coming from the restrictor RE takes place. The data measured are the temperatures and pressures at the inlet into the compressor (t1h, p0) and at the outlet from the compressor (t2h, pc), the effective volume flow Veff and the rotational speed of the compressor shaft.
The composition according to the invention, which contains R23 and R134a and which forms a non-azeotropic mixture, was additionally subjected in a known manner to p-v-T-x measurements according to the isochor principle. Taking into account the volumetric behavior data, obtained from the p-v-T-x measurements, of the composition according to the invention, and the test results on the compressor test stand, it was possible to determine or calculate, in a known manner via the compilation of the Mollier diagram, the following refrigeration characteristics for the refrigerant composition according to the invention:
______________________________________
Evaporation temperature (t.sub.o)
-39.8 to -27° C.
Pressure at the compressor inlet (p.sub.o)
1.05 bar
Temperature at the compressor inlet
1.82° C.
(t.sub.1h)
Pressure at the compressor outlet (p.sub.c)
10.60 bar
Temperature at the compresser outlet
97.73° C.
(t.sub.2h)
Liquefaction temperature (t.sub.c)
38.5 to 25.6° C.
Effective refrigerant volume flow (V.sub.eff)
6.37 m.sup.3 /h
Performarice coefficient of the
η.sub.RE
2.10
refrigeration process
Volumetric efficiency
λ
0.698
Isentropic compression efficiency
η.sub.is
0.716
Refrigerating capacity
Q.sub.o
1.37 kW
Pressure ratio p.sub.c /p.sub.o
10.1
Refrigerant mass flow
m.sub.R
29.68 kg/h
______________________________________
The data determined on the basis of experimental measurements documents the useful refrigeration characteristics of the compositions according to the invention comprising R23 and R134a. Using the refrigerant compositions according to the invention, a high refrigerating capacity and a high performance coefficient are achieved at an acceptable pressure ratio.
The foregoing description and examples have been set forth merely to illustrate the invention and are not intended to be limiting. Since modifications of the disclosed embodiments incorporating the spirit and substance of the invention may occur to persons skilled in the art, the invention should be construed to include everything within the scope of the appended claims and equivalents thereof.
Claims (6)
1. A composition useful as a refrigerant in refrigerating machines and air-conditioning systems, consisting of from 2 to 8% by weight trifluoromethane and from 92 to 98% by weight 1,1,1,2-tetrafluoroethane.
2. A composition according to claim 1, which consists of from 4 to 6% by weight trifluoromethane and from 94 to 96% by weight 1,1,1,2-tetrafluoroethane.
3. In a method of refrigeration wherein a refrigerant is circulated between a heat absorbing station and a heat releasing station, the improvement comprising using as said refrigerant a composition consisting of from 2 to 8% by weight trifluoromethane and from 92 to 98% by weight 1,1,1,2-tetrafluoroethane.
4. A method according to claim 3, wherein said refrigerant composition consists of from 4 to 6% by weight trifluoromethane and from 94 to 96% by weight 1,1,1,2-tetrafluoroethane.
5. A method according to claim 3, wherein said heat absorbing station is maintained at a refrigerant evaporation temperature of below -25° C.
6. A method according to claim 5, wherein said heat absorbing station is maintained at a refrigerant evaporation temperature of between -25° C. and -45° C.
Applications Claiming Priority (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| DE4222855A DE4222855A1 (en) | 1992-07-11 | 1992-07-11 | New refrigerant compositions |
| DE4222855.7 | 1992-07-11 |
Publications (1)
| Publication Number | Publication Date |
|---|---|
| US5429760A true US5429760A (en) | 1995-07-04 |
Family
ID=6462999
Family Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| US08/089,829 Expired - Fee Related US5429760A (en) | 1992-07-11 | 1993-07-12 | Refrigerant composition containing trifluoromethane and 1,1,1,2-tetrafluoroethane |
Country Status (26)
| Country | Link |
|---|---|
| US (1) | US5429760A (en) |
| EP (1) | EP0579072B1 (en) |
| JP (1) | JPH06166868A (en) |
| KR (1) | KR940002338A (en) |
| CN (1) | CN1081460A (en) |
| AR (1) | AR247910A1 (en) |
| AT (1) | ATE133444T1 (en) |
| AU (1) | AU663783B2 (en) |
| BR (1) | BR9302818A (en) |
| CA (1) | CA2100316A1 (en) |
| CZ (1) | CZ102293A3 (en) |
| DE (2) | DE4222855A1 (en) |
| ES (1) | ES2082559T3 (en) |
| FI (1) | FI933155A (en) |
| HU (1) | HUT67329A (en) |
| IL (1) | IL105948A (en) |
| JO (1) | JO1752B1 (en) |
| LT (1) | LT3082B (en) |
| LV (1) | LV10787B (en) |
| MX (1) | MX9304121A (en) |
| MY (1) | MY109007A (en) |
| PL (1) | PL299632A1 (en) |
| SI (1) | SI9300371A (en) |
| SK (1) | SK56393A3 (en) |
| TR (1) | TR26928A (en) |
| TW (1) | TW290585B (en) |
Cited By (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5705086A (en) * | 1996-04-16 | 1998-01-06 | Mobil Oil Corporation | Refrigeration oils comprising esters of hindered alcohols |
| US6176102B1 (en) * | 1998-12-30 | 2001-01-23 | Praxair Technology, Inc. | Method for providing refrigeration |
| US6327866B1 (en) | 1998-12-30 | 2001-12-11 | Praxair Technology, Inc. | Food freezing method using a multicomponent refrigerant |
| WO2003027206A2 (en) * | 2001-09-25 | 2003-04-03 | American Standard International Inc. | Replacement refrigerant for r410a |
| US20040061091A1 (en) * | 2002-10-01 | 2004-04-01 | Tieken James B. | Refrigerant blend |
Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0430170A1 (en) * | 1989-11-30 | 1991-06-05 | Matsushita Electric Industrial Co., Ltd. | Working fluid |
| EP0430130A1 (en) * | 1989-11-29 | 1991-06-05 | Matsushita Electric Industrial Co., Ltd. | Working fluid |
| JPH03170591A (en) * | 1989-11-30 | 1991-07-24 | Matsushita Electric Ind Co Ltd | Working fluid |
| JPH0496989A (en) * | 1990-08-10 | 1992-03-30 | Sanyo Electric Co Ltd | Refritgerant composition and refrigerator |
| JPH0532961A (en) * | 1991-07-25 | 1993-02-09 | Daikin Ind Ltd | Mixed cooling medium containing trifluoromethane |
| TW204364B (en) | 1992-03-05 | 1993-04-21 | Dairei Kk | Carbon-fluoro coolant mixture |
Family Cites Families (4)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5304319A (en) * | 1989-11-30 | 1994-04-19 | Matsushita Electric Industrial Co., Ltd. | Working fluid |
| JPH0655943B2 (en) * | 1989-11-30 | 1994-07-27 | 松下電器産業株式会社 | Working fluid |
| JP2580350B2 (en) * | 1989-11-30 | 1997-02-12 | 松下電器産業株式会社 | Working fluid |
| WO1993015163A1 (en) * | 1992-02-03 | 1993-08-05 | Allied-Signal Inc. | Novel refrigerant compositions |
-
1992
- 1992-07-11 DE DE4222855A patent/DE4222855A1/en not_active Withdrawn
-
1993
- 1993-05-28 CZ CZ931022A patent/CZ102293A3/en unknown
- 1993-06-04 SK SK563-93A patent/SK56393A3/en unknown
- 1993-06-04 TW TW082104480A patent/TW290585B/zh active
- 1993-06-08 IL IL10594893A patent/IL105948A/en not_active IP Right Cessation
- 1993-06-09 AU AU40122/93A patent/AU663783B2/en not_active Ceased
- 1993-06-25 AR AR93325271A patent/AR247910A1/en active
- 1993-07-01 JO JO19931752A patent/JO1752B1/en active
- 1993-07-02 KR KR1019930012442A patent/KR940002338A/en not_active Application Discontinuation
- 1993-07-05 HU HU9301945A patent/HUT67329A/en unknown
- 1993-07-05 EP EP93110681A patent/EP0579072B1/en not_active Expired - Lifetime
- 1993-07-05 ES ES93110681T patent/ES2082559T3/en not_active Expired - Lifetime
- 1993-07-05 AT AT93110681T patent/ATE133444T1/en not_active IP Right Cessation
- 1993-07-05 DE DE59301495T patent/DE59301495D1/en not_active Expired - Fee Related
- 1993-07-07 TR TR00648/93A patent/TR26928A/en unknown
- 1993-07-08 CN CN93108689A patent/CN1081460A/en active Pending
- 1993-07-08 MX MX9304121A patent/MX9304121A/en not_active Application Discontinuation
- 1993-07-09 LT LTIP773A patent/LT3082B/en not_active IP Right Cessation
- 1993-07-09 FI FI933155A patent/FI933155A/en not_active Application Discontinuation
- 1993-07-09 JP JP5170158A patent/JPH06166868A/en active Pending
- 1993-07-09 BR BR9302818A patent/BR9302818A/en not_active Application Discontinuation
- 1993-07-09 MY MYPI93001347A patent/MY109007A/en unknown
- 1993-07-09 LV LVP-93-987A patent/LV10787B/en unknown
- 1993-07-09 PL PL29963293A patent/PL299632A1/en unknown
- 1993-07-09 SI SI9300371A patent/SI9300371A/en unknown
- 1993-07-12 CA CA002100316A patent/CA2100316A1/en not_active Abandoned
- 1993-07-12 US US08/089,829 patent/US5429760A/en not_active Expired - Fee Related
Patent Citations (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| EP0430130A1 (en) * | 1989-11-29 | 1991-06-05 | Matsushita Electric Industrial Co., Ltd. | Working fluid |
| EP0430170A1 (en) * | 1989-11-30 | 1991-06-05 | Matsushita Electric Industrial Co., Ltd. | Working fluid |
| JPH03170591A (en) * | 1989-11-30 | 1991-07-24 | Matsushita Electric Ind Co Ltd | Working fluid |
| JPH0496989A (en) * | 1990-08-10 | 1992-03-30 | Sanyo Electric Co Ltd | Refritgerant composition and refrigerator |
| JPH0532961A (en) * | 1991-07-25 | 1993-02-09 | Daikin Ind Ltd | Mixed cooling medium containing trifluoromethane |
| TW204364B (en) | 1992-03-05 | 1993-04-21 | Dairei Kk | Carbon-fluoro coolant mixture |
Non-Patent Citations (4)
| Title |
|---|
| DATABASE WPI Section Ch, Week 9220, Derwent Publications Ltd., London, GB; Class E16, AN 1992-162202 & JP-A-04 096 989 (SANYO ELECTRIC CO) 30. März 1992 * |
| Derwent Abstract of JP 04/096,989, Mar. 1992. |
| Pannock et al, "Performance of Chlorine-free Binary Zeotropic Refrigerant Mixtures", Chem. Abs. 119((22):228807e, Dec. 1991. |
| Pannock et al, Performance of Chlorine free Binary Zeotropic Refrigerant Mixtures , Chem. Abs. 119((22):228807e, Dec. 1991. * |
Cited By (6)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US5705086A (en) * | 1996-04-16 | 1998-01-06 | Mobil Oil Corporation | Refrigeration oils comprising esters of hindered alcohols |
| US6176102B1 (en) * | 1998-12-30 | 2001-01-23 | Praxair Technology, Inc. | Method for providing refrigeration |
| US6327866B1 (en) | 1998-12-30 | 2001-12-11 | Praxair Technology, Inc. | Food freezing method using a multicomponent refrigerant |
| WO2003027206A2 (en) * | 2001-09-25 | 2003-04-03 | American Standard International Inc. | Replacement refrigerant for r410a |
| WO2003027206A3 (en) * | 2001-09-25 | 2004-03-04 | American Standard Int Inc | Replacement refrigerant for r410a |
| US20040061091A1 (en) * | 2002-10-01 | 2004-04-01 | Tieken James B. | Refrigerant blend |
Also Published As
| Publication number | Publication date |
|---|---|
| AR247910A1 (en) | 1995-04-28 |
| FI933155A (en) | 1994-01-12 |
| CA2100316A1 (en) | 1994-01-12 |
| LV10787A (en) | 1995-08-20 |
| HU9301945D0 (en) | 1993-09-28 |
| HUT67329A (en) | 1995-03-28 |
| AU663783B2 (en) | 1995-10-19 |
| TW290585B (en) | 1996-11-11 |
| EP0579072B1 (en) | 1996-01-24 |
| TR26928A (en) | 1994-08-24 |
| LV10787B (en) | 1996-06-20 |
| JO1752B1 (en) | 1993-10-30 |
| BR9302818A (en) | 1994-02-16 |
| AU4012293A (en) | 1994-01-13 |
| ES2082559T3 (en) | 1996-03-16 |
| LTIP773A (en) | 1994-07-15 |
| MX9304121A (en) | 1994-03-31 |
| KR940002338A (en) | 1994-02-17 |
| PL299632A1 (en) | 1994-02-21 |
| MY109007A (en) | 1996-11-30 |
| JPH06166868A (en) | 1994-06-14 |
| FI933155A0 (en) | 1993-07-09 |
| ATE133444T1 (en) | 1996-02-15 |
| SK56393A3 (en) | 1994-05-11 |
| DE4222855A1 (en) | 1994-01-13 |
| LT3082B (en) | 1994-11-25 |
| EP0579072A1 (en) | 1994-01-19 |
| CZ102293A3 (en) | 1994-02-16 |
| SI9300371A (en) | 1994-03-31 |
| DE59301495D1 (en) | 1996-03-07 |
| CN1081460A (en) | 1994-02-02 |
| IL105948A0 (en) | 1993-10-20 |
| IL105948A (en) | 1996-06-18 |
Similar Documents
| Publication | Publication Date | Title |
|---|---|---|
| Kim et al. | Experiment and simulation on the performance of an autocascade refrigeration system using carbon dioxide as a refrigerant | |
| Zhang et al. | Experimental investigation of the performance of an R1270/CO2 cascade refrigerant system | |
| US6063305A (en) | Refrigerant compositions containing a hydrofluoropropane and a hydrofluorocarbon | |
| US5360566A (en) | Hydrocarbon refrigerant for closed cycle refrigerant systems | |
| Jung et al. | Performance simulation of a two-evaporator refrigerator—freezer charged with pure and mixed refrigerants | |
| Sarkar | Transcritical CO2 refrigeration systems: comparison with conventional solutions and applications | |
| Chen et al. | Simulation of a vapour-compression refrigeration cycles using HFC134a and CFC12 | |
| Bolaji | Experimental analysis of reciprocating compressor performance with eco-friendly refrigerants | |
| US5429760A (en) | Refrigerant composition containing trifluoromethane and 1,1,1,2-tetrafluoroethane | |
| AU593979B2 (en) | Refrigerant and a machine having a refrigerating circuit with refrigerant | |
| Yi et al. | Exergy characteristics of R404A indirect refrigeration system using CO 2 as a secondary refrigerant | |
| Li et al. | Experimental study of a series-connected two-evaporator refrigerating system with propane (R-290) as the refrigerant | |
| CN112745804A (en) | Low-temperature mixed working medium and application thereof | |
| Ouadha et al. | Performance comparison of cascade and two-stage refrigeration cycles using natural refrigerants | |
| Bisht et al. | Thermodynamic analysis of actual vapour compression system with R12 and its eco-friendly alternatives refrigerants | |
| Kılıç et al. | International Journal of Energy Applications and Technologies | |
| CN115584241A (en) | Mixed refrigerant, refrigerating system and refrigerator | |
| Dang et al. | An Experimental Study on The Performance of An Air Conditioning System using CO 2 Refrigerant with The Actual Power Input of 440W | |
| Dang et al. | Effect of the Pressure Ratio on the Heat Transfer Phenomena of the Evaporator in CO2 Air Conditioning System | |
| Domanski | Byung Soon Kim, LG Electronics, Changwon City, 641-315 Korea | |
| Siva et al. | Performance Analysis of Eco-Friendly HC Mixture (R290/R600a) Refrigerant as an Alternative to R-134a in a Vapour Compression Refrigeration System for Subcooling using Heat Exchanger at Condenser Outlet and Diffuser at Condenser Inlet | |
| EP4328283A2 (en) | Refrigeration systems and methods | |
| Hoff | Performance analysis of CO2 refrigeration systems in Nordic supermarkets | |
| Ma et al. | Experimental performance of TJR02 as an alternative refrigerant to R22 in a small-scale cold storage | |
| JPH06317358A (en) | Refrigerator |
Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| AS | Assignment |
Owner name: SOLVAY FLUOR UND DERIVATE GMBH, GERMANY Free format text: ASSIGNMENT OF ASSIGNORS INTEREST;ASSIGNORS:DORING, REINHOLD;BUCHWALD, HANS;VON EYNATTEN, CHRISTOPH;REEL/FRAME:006675/0890;SIGNING DATES FROM 19930621 TO 19930713 |
|
| AS | Assignment |
Owner name: SOLVAY FLUOR UND DERIVATE GMBH, GERMANY Free format text: CORRECTIV;ASSIGNORS:DOERING, REINHOLD;BUCHWALD, HANS;VON EYNATTEN, CHRISTOPH;REEL/FRAME:006818/0054;SIGNING DATES FROM 19930621 TO 19930713 |
|
| REMI | Maintenance fee reminder mailed | ||
| LAPS | Lapse for failure to pay maintenance fees | ||
| FP | Lapsed due to failure to pay maintenance fee |
Effective date: 19990704 |
|
| STCH | Information on status: patent discontinuation |
Free format text: PATENT EXPIRED DUE TO NONPAYMENT OF MAINTENANCE FEES UNDER 37 CFR 1.362 |